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A core-shell honeycomb catalyst for denitrification and anti-thallium poisoning of cement kiln flue gas and its preparation method

A core-shell catalyst and core-shell honeycomb technology, applied in the field of denitration catalysts, can solve the problems of short life, poor activity, and rapid reduction of denitration efficiency, and achieve the effects of prolonging life, prolonging service life, and improving denitration efficiency and activity.

Active Publication Date: 2021-09-24
JIANGSU LONGKING COALOGIX CATALYST REGENERATION CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In view of the above problems, the present invention proposes a cement kiln flue gas denitrification anti-thallium poisoning core-shell honeycomb catalyst and its preparation method, which overcomes the rapid reduction in catalyst denitrification efficiency and poor activity of the denitrification catalyst in the prior art in thallium-containing flue gas , the problem of short life

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] A method for preparing a cement kiln flue gas denitration and anti-thallium poisoning core-shell honeycomb catalyst, comprising the following steps:

[0029] 1) V-W / TiO with antithallium additive added 2 Preparation: Add 0.370kg of ammonium metavanadate, 1.25kg of ammonium metatungstate, and 0.36kg of gallium oxide into deionized water, stir and heat to dissolve, then add 18.36kg of commercial titanium dioxide powder, and continue stirring under ultrasonic conditions to obtain a slurry The material is injected into a spray dryer and dried at a drying temperature of 150°C to obtain a 2% Ga / V-W / TiO 2 powder;

[0030] 2) V-W / TiO 2 @Metal oxide core-shell catalyst preparation: take 2% Ga / V-W / TiO 2 Powder 2kg, ultrasonically dispersed in ethanol / water (v / v=1) mixed solution to obtain a suspension, then add 10kgPVP to the suspension and continue ultrasonic until the dispersion is uniform, then add 0.34kg of tetraethyl orthosilicate and 0.2kg of hexamethylenetetramine, aft...

Embodiment 2

[0033] A method for preparing a cement kiln flue gas denitration and anti-thallium poisoning core-shell honeycomb catalyst, comprising the following steps:

[0034] 1) V-W / TiO with antithallium additive added 2 Preparation: Add 0.30kg of ammonium metavanadate, 1.30kg of ammonium metatungstate, and 0.72kg of indium oxide into deionized water. After fully stirring and heating to dissolve, add 18kg of commercial titanium dioxide powder, and continue stirring under ultrasonic conditions to obtain a slurry , injected into a spray dryer and dried at a drying temperature of 300°C to obtain a 4% In / V-W / TiO 2 powder;

[0035] 2) Preparation of V-W / TiO2@metal oxide core-shell catalyst: take 4% In / V-W / TiO 2 Powder 1.96kg, ultrasonically dispersed in ethanol / water (v / v=3) mixed solution to obtain a suspension, then add 9.8kgPVP to the suspension and continue ultrasonic until uniformly dispersed, then add ammonium molybdate 0.18kg and 0.3kg of hexamethylenetetramine, after condensing an...

Embodiment 3

[0038]A method for preparing a cement kiln flue gas denitration and anti-thallium poisoning core-shell honeycomb catalyst, comprising the following steps:

[0039] 1) V-W / TiO with antithallium additive added 2 Preparation: Add 0.27kg of ammonium metavanadate, 1.35kg of ammonium metatungstate, and 0.6kg of gallium sulfate into deionized water. After fully stirring and heating to dissolve, add 20kg of commercial titanium dioxide powder, and continue stirring under ultrasonic conditions to obtain a slurry , injected into a spray dryer and dried at 200°C to obtain 3% Ga / V-W / TiO 2 powder;

[0040] 2) V-W / TiO 2 @Metal oxide core-shell catalyst preparation: take 3% Ga / V-W / TiO 2 Powder 1.98kg, ultrasonically dispersed in ethanol / water (v / v=2) mixed solution to obtain a suspension, then add 9.5kgPVP to the suspension and continue ultrasonic until uniformly dispersed, then add 0.31kg of zirconium acetate and 0.3 kg hexamethylenetetramine, after reflux, the product was cooled to room...

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Abstract

The invention discloses a core-shell honeycomb catalyst used for cement kiln flue gas denitrification and anti-thallium poisoning and a preparation method thereof. The catalyst is a core-shell catalyst, with V-W / TiO2 added with an anti-thallium additive as the core structure, and a metal oxide film as the shell structure; the anti-thallium additive includes elemental gallium and / or elemental indium. The anti-thallium poisoning ability of the denitrification catalyst prepared by the invention is 2 to 3 times higher than that of the existing catalysts, and the denitrification efficiency is kept stable above 90%, realizing the breakthrough of the denitrification catalyst technology under the condition of thallium-containing flue gas in cement kilns. The catalyst of the invention can prolong the service life of the SCR denitration catalyst, reduce the use cost of the denitration system, improve the adaptability of the SCR denitration catalyst under the condition of thallium-containing flue gas, reduce the production cost of denitration operation management, and has great economic value.

Description

technical field [0001] The invention belongs to the technical field of denitrification catalysts, and relates to a core-shell honeycomb catalyst for denitrification and anti-thallium poisoning of cement kiln flue gas and a preparation method thereof. Background technique [0002] Nitrogen oxides are an important pollutant in air pollution, and the treatment of nitrogen oxides in coal power plants has matured to meet the requirements of ultra-low emissions. Cement kiln flue gas nitrogen oxide is the third largest pollution source after thermal power and automobile exhaust. At present, SCR denitrification technology is one of the most widely used and most mature and effective flue gas denitrification technologies. The SCR denitrification device of coal-fired power plant is mainly installed between the economizer and the air preheater, and contains a large amount of fly ash and high concentration of SO 2 Gas, after running for 24000 hours, the SCR catalyst will be deactivated...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/30B01J35/04B01D53/90B01D53/56
CPCB01J23/30B01D53/90B01D53/8628B01J35/56
Inventor 张涛刘安阳邓立锋罗春云任英杰
Owner JIANGSU LONGKING COALOGIX CATALYST REGENERATION CO LTD